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Eprints ID : 16806
To link to this article : DOI : 10.1016/j.porgcoat.2013.12.013
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http://dx.doi.org/10.1016/j.porgcoat.2013.12.013
To cite this version :
Musiani, Marco and Orazem, Mark E. and
Pébère, Nadine and Tribollet, Bernard and Vivier, Vincent
Determination of resistivity profiles in anti-corrosion coatings from
constant-phase-element parameters. (2014) Progress in Organic
Coatings, vol. 77 (n° 12). pp. 2076-2083. ISSN 0300-9440
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Determination
of
resistivity
profiles
in
anti-corrosion
coatings
from
constant-phase-element
parameters
M.
Musiani
a,
M.E.
Orazem
b,
N.
Pébère
c,∗,
B.
Tribollet
d,
V.
Vivier
d aIstitutoperl’EnergeticaeleInterfasi,ConsiglioNazionaledelleRicerche,35127Padova,ItalybDepartmentofChemicalEngineering,UniversityofFlorida,FL32611,USA
cUniversitédeToulouse,CIRIMAT,UPS/INPT/CNRS,ENSIACET,4,alléeEmileMonso–BP44362,31030Toulousecedex4,France dLaboratoireInterfacesetSystèmesElectrochimiques,UPR15duCNRS,UniversitéPierreetMarieCurie,75252Pariscedex05,France
Keywords: CPE Electrolyteuptake Impedancemodelling Pores
a
b
s
t
r
a
c
t
ArecentlyproposedmodelwhichexplainstheCPEresponseexhibitedbymetal/coating/electrolyte sys-temsastheresultofpower-lawdependencesofthecoatingresistivityandpermittivityalongtheir thicknessisrevisitedandappliedtothreedifferentcoating/electrolytecombinations.Itisshownthat resistivityprofilesmaybedetermined,andtheirevolutionwiththetimeofexposuremaybefollowed. Theeffectoftheassumptionsmadeoncoatingandelectrolyteresistivityontheregressedparameters isdiscussedandthefactorswhichaffectthereliabilityofthemeasuredwateruptakearehighlighted. Itisshownthatboththecompositionofthecoatingandthatofthetestsolutionsinfluencethetime dependenceofthecoatingperformance.
1. Introduction
Electrochemicalimpedancespectroscopyisapopulartechnique for the assessment of the corrosion protection performance of organiccoatings.Theanalysisofimpedancedataisoftenbasedon theequivalentcircuitproposedbyBeaunieretal.[1]inwhichthe coatingcapacityandthedoublelayercapacityarereplacedby con-stantphaseelements(CPE),theimpedanceofwhichisZ=1/(jω)˛Q.
SubstitutionofCPEsforcapacitiesmaystronglyimprovethe qual-ityofthefittingbetweentheexperimentaldataandtheequivalent circuit,butcreatesambiguitiesinthephysicalinterpretationofthe results,sinceQcannotbesimplyidentifiedwiththecoating capac-ity[2]andcannotbedirectlyusedtocalculatethewateruptakein thecoatingthroughtheBrasherandKingsbury[3]approach. Vari-ousformulashavebeenproposedforthecalculationoftheeffective capacityfromCPEparameters[4,5],buttheirapplicationrequires knowledgeofthephysicaloriginoftheCPEbehaviour[2,6].
In a recent paper [7], our group has shown that the CPE behaviour observed in theimpedance of a coated systemmay beexplainedby aninhomogeneouselectrolyteuptake if(i)the electrolytevolumefractiondecreasesfromthecoating/electrolyte interfacetothemetal/coatinginterfaceaccordingtoapower-law and(ii)theresistivityandpermittivityofthesystemarecalculated usingeffectivemediumtheoryformulascorrespondingtoa par-allelcombinationofcoatingmaterialandelectrolyte.Thismodel,
∗ Correspondingauthor.Tel.:+33534323423;fax:+33534323499.
E-mailaddress:Nadine.Pebere@ensiacet.fr(N.Pébère).
henceforth briefly called “power-law model”was compared to experimentaldataobtainedwithahybridsol–gelcoatingexposed toa0.5MNaClsolution.Itwasconcludedthat,asaresultofthe progressiveelectrolyteuptake forincreasingexposuretime, the resistivityofthecoatingmarkedlydecreased(afteroneweek,the decreaseatthecoating/electrolyteinterfaceattainedca.6ordersof magnitude,withrespecttothedrycoating),whileitspermittivity remainedpracticallyunchanged.Furthermore,itwasshownthat thenumberand/orsectionofthethroughpores,i.e.poresasdeep asthewholecoatingthickness,directlyconnectingtheelectrolyte withthemetalunderneaththecoatingthroughalow-resistance path, increased with exposure time. These results allowed the extension ofa previously derived model [8,9]appliedso farto passiveoxidesandhumanskin[10],toanti-corrosioncoatings.
Thepresentpaperaimsatextendingtheinvestigationdescribed inRef. [7],focusingmainlyonthreeissues:(i)theeffectof the assumptions madeoncoating and electrolyteresistivity onthe regressed parameters; (ii)the analysis of the relative amounts of electrolytewithin throughand shortpores; (iii) theanalysis ofexperimentaldatarelevanttoothercoating/electrolyte combi-nations,basedonthepower-lawmodel,andadiscussionofthe differentbehaviourofdifferentsystems.
2. Experimental
Adescriptionofthecoatings,theirmethodofpreparation,and theelectrochemicaltechniquesusedfortheircharacterizationare presentedinthissection.
ξ = 1 ξ = 0 Electrolyte Coang Substrate ρ(ξ) ε(ξ) Rpore Re CPE Oxide Zc
Fig.1.Schematicrepresentationofasubstrate/oxide/coating/electrolytesystem.Reistheuncompensatedelectrolyteresistance;Rporeaccountsforthethroughporesjoining
thecoating/electrolyteandcoating/oxideinterface;Zcistheimpedanceoftheelectrolyte-penetratedcoatingdescribedbyEq.(3);theCPErepresentstheoxidelayercovering
theAl2024alloy.
2.1. Hybridsol–gelcoatings
Twocoatingswereprepared.Forbothsystems,the organosilox-ane sol was prepared by using 3-glycidoxypropylethoxysilane (GLYEO),tetraethylorthosilicate(TEOS)andbutanol.Afirst solu-tionwasmadebyaddingapolyaminoamide(PAA)tothesol,with aGLYEO/TEOS/PAAmassratioof3:1:2.Thesolutionwasprepared withanexcessoforganosilane,thereforetheresultingcoatingwas calledO.Theprocesstakesadvantageofthetwomoietiesofthe organosilane molecule(GLYEO). Theorganicpart of theGLYEO reactswiththeaminefunctionsofthePAAtodeveloptheorganic partofthehybridcoating,whilethesilanepartundergoestheusual hydrolysisandcondensationstepsofsol–gelsynthesis,toforma silicon-basednetwork.TEOSwasaddedtoincreasethecoating den-sity.Inthesecondsolution,anepoxycompoundwasaddedtothe firstsolution,withaGLYEO/TEOS/PAA/Epoxyratioof1:1:10:8.Due tothepresenceofanepoxyinthesolution,theresultingcoating wascalledsampleE.Theadditionoftheepoxycompoundinthe liq-uidsol–gelresinrequiredadifferentprocedureformixingtogether thecompounds.Forthisreason,sampleEisnotcomparable,from achemicalpointofview,withsampleO.Thesol–gelfilmsdidnot containanypigmentsorfillers.
Thecoatingsweredepositedontoa2024T3aluminiumalloy currentlyusedintheaerospaceindustry.Thespecimensconsisted of125mm×80mm×1.6mmplatesmachinedfromrolledplate. Beforepainting,thesamplesweredegreasedat60◦C(pH=9)for
15min,rinsedtwicewithdistilledwater,thenetchedinanacid bathat52◦Cfor10min,andrinsedagainwithdistilledwater.The
liquidpaintswereappliedbyairsprayingandcuredat100◦Cfor
1h.Thecoatingsthicknesswasmeasuredatseverallocationsfrom theobservationofthecross-sectionsofthesamplesbySEMand foundtohaveanaveragevalueof20±2mm.
2.2. Electrochemicalimpedancemeasurements
Athree-electrodeelectrochemicalcellwasusedinwhichthe coated specimenservedas theworkingelectrode. Acylindrical Plexiglastubewasassembledontopofthecoatedsample, expos-ingasurfaceareaof24cm2.Alargeplatinumsheetwasusedas
counter-electrode.Asaturatedmercury/mercuroussulphate ref-erence electrode was used for electrolytes containing Na2SO4,
and a saturated calomel reference electrode wasused in elec-trolytes containing NaCl. The electrochemical cell wasopen to air and was kept at room temperature withan average value of 17◦C and which may have undergonefluctuations by±2◦C.
Followingourpreviouswork,theresultingvariationsinthe dielec-tric constant of water were unlikely to have significanteffects on the experimental impedance response [9]. Electrochemical impedancemeasurementswerecarriedoutusingaBiologicVSP apparatus.Theimpedancediagramswereobtainedunder potentio-staticconditionsatthecorrosionpotentialoverafrequencyrange of60kHz–10mHzwith6pointsperdecade,usinga20mV peak-to-peaksinusoidalvoltage.Theelectrochemicalbehaviourofthe coatingswascharacterizedineither0.5MNa2SO4 or0.5MNaCl,
forexposuretimesrangingfrom2hto168h.TheNa2SO4solution
wasusedtoachieveabetterknowledgeoftheintrinsic proper-tiesofthecoatingsbecausetheevolutionofthesystemwasslower thaninNaClsolution.TheresultsconcerningsampleEintheNaCl solutionwerepreviouslyreportedinRef.[7].
3. Modelfordataanalysis
Themodelemployedforthedataanalysishasbeenpreviously described [7];onlya briefsummaryis reportedhere.Ascheme ofasubstrate/oxide/coating/electrolytesystem,anditsequivalent circuit,arepresentedinFig.1.Theimpedanceisassumedtoconsist ofthreecomponentsconnectedinseries:
i.theuncompensatedelectrolyteresistance; ii.theimpedanceofthecoating,discussedbelow;
iii.theimpedance oftheoxidecovering theAl2024alloy;this impedanceisaccountedforbyaconstantphaseelement(CPE) andisnolongerdiscussedinthefollowing.
Thecoatingisassumedtobepenetratedbytheelectrolytewhich fillsitspores.TheseporesarerepresentedinFig.1asbeingstraight, althoughtheymaybetortuousandhavevariablelateral dimen-sion.Allporeshaveamouthatthecoating/electrolyteinterface, butonlyafew(henceforthcalled“throughpores”)areasdeepas thecoatingandreachthecoating/oxideinterface,providinga low-resistivitypath,withresistanceRpore,betweentheelectrolyteand theoxide.Theotherpores(henceforthcalled“shortpores”)areless deepthanthecoatingthicknessı,andthusdifferentplanesparallel totheinterfaces,locatedwithinthecoatingatdifferentpositions =x/ı,crossdifferentnumbersofpores(seesketchinFig.2),and differentelementallayersofthecoating,dthick,havedifferent localelectrolytevolumefractions().Sucharepresentationofthe electrolyte-penetratedcoatingisinagreementwiththeone pro-posedbyMiˇskovi ´c-Stankovi ´cetal.[11,12]onthebasisofoptical microscopycoupledwithimageanalysis.
Fig.2. Schematicrepresentationofthinlayersofthecoatingmateriallocatedat differentpositions,highlightingthatthenumberofporesdecreasesasbecomes smaller,i.e.asthedistancefromthecoating/electrolyteinterfaceincreases.
Theelectrolytevolumefractionaffectsthelocalresistivityand permittivityofthecoating,whichareexpressedthrougheffective mediumtheoryformulasas
()−1=−1w()+−1c [1−()] (1)
and
ε()=εw()+εc[1−()] (2)
wherethesubscriptswandcrefertotheelectrolyteandthe coat-ingmaterial,respectively.Eqs.(1)and(2)takeintoaccountthat, ineachelementallayerparalleltotheinterfaces,eachpositionis occupiedbyeitherthecoatingmaterialortheelectrolyte,andso thesetwomediaareinparalleltoeachother.Inthis approxima-tionitisunimportantwhether()istheresultofthepresenceof alargenumberofsmallerporesorasmallnumberoflargerpores. However,()doesnottakeintoaccountthewaterpresentwithin thecoatingasindividualmoleculesinteractingwithpolymeric net-workandnotformingaggregatesbigenoughtoallowdissolution ofsaltsandgenerateaconductivemedium.Suchpolymer-bounded waterhasbeenreportedtobea verysignificantfractionofthe totalwater uptakenbyepoxycoatings[11]andtocausestrong plasticizationofanepoxy/polyamidoaminecoating[13].Therefore, thewateruptakedeterminedthroughtheanalysisofexperimental databycomparisonwiththemodelproposedinRef.[7]islikely tobeunderestimated.Inafollowingsection(seeSection4.1.3),it willbediscussedhowalowerresistivityoftheelectrolytewithin thepores,ascomparedtothatoftheexternalsolution,maybea furthercauseforunderestimatingthewateruptake.
Under assumption that each elemental layermay be repre-sented by a parallel combination of a resistance ()d and a capacitanceε()ε0/d,theimpedanceoftheelectrolyte-penetrated
coating(Zc)iscalculatedas Zc(ω)=ı 1
Z
0 1 ()−1+jωε()ε0d (3)Thecontributionofporesthatextendtotheoxidesurfaceis includedseparatelyfromthedevelopmentofEq.(3).Theoverall
impedanceZ(ω)ofthecoatingistherebygivenbythepore resis-tanceRporeinparallelwithZc,i.e.
Z(ω)=[Zc(ω)−1+R−1 pore]
−1
(4) Toaccountfortheprogressivevariationinthenumberofpores along the coating thickness, the hypothesis is made that () changesfrom(0)=0at=0to(ı)at=1accordingtoa power-law,i.e.,
()= (ı)
1+(ı)( −1) (5)
ThecoatingpartcorrespondingtotheimpedanceZc contains only“shortpores”,meaningthatnoelectrolytereachesthe inter-facebetweenthecoating andtheoxideand, asa consequence, (0)=0.
In Ref. [7], calculated impedanceplots were presented with (ı)andRpore asparameters.It wasshownthat,accordingtoa moregeneraltheoryreportedinRef.[8],Z(ω)correspondedtoa CPEbehaviour,withaCPEexponent ˛linkedtothepower-law exponent bytheequation
˛= −1
(6)
ItwasshowninRef.[7]thatfittingtheabovedescribedmodel toexperimentaldataalloweddeterminationof ,(ı),andRpore, byassumingknownorreasonablevaluesforw,c,εwandεc.The ()−profileswerecalculatedbyenteringthefitted and(ı) valuesintoEq.(5);hence,()−profilescorrespondingto differ-entimmersiontimeswereobtainedthroughEq.(1).Theseprofiles, presentedinRef.[7],neglectedthethroughpores,and,therefore,at allimmersiontimes,(0)wasidenticaltoc.Inthepresentpaper, theelectrolytecontentinthethroughporesiscalculatedas ϕpore=Vpore Vfilm = Apore Afilm = ıw RporeAfilm (7) where Vdenotes a volume, and Ais a surface area(with Rpore normalizedtounitsurfaceareaandAfilm=1cm2).Thisallows esti-mationofthefractionoftheuptakenelectrolytethatiscontained inthethroughporesandcalculationof()−profiles,takinginto accountallpores.Owingtotheassumedcylindricalgeometryof thethroughpores,Rporeisnotafunctionofposition.
Theabovedevelopmentretainsthemeaningof(0)asthe resis-tanceof thedrycoating,c.Asmaybeseenin thesubsequent discussionofexperimentalresults,thepower-lawmodeldoesnot accountadequatelyforthehigh-frequencyresponse.Theoriginof thisdiscrepancyis,asyet,unknown.Atentativeexplanationmight invokecapacitiveinteractionsbetweenadjacentpores.The regres-sionanalysiswastherefore performedfor frequenciesuptoan upperlimitwhich,fordifferentsystems,variedfrom0.5to5kHz (seeFigs.3and6).
4. Resultsanddiscussion
Theresultsarepresentedintermsoftheinfluenceofassumed valuesforparametersw,c,εwandεconthefittedparameters,the relativeamountsofelectrolytewithinthroughandshortpores,and theinfluenceofcoatingformulationandelectrolytecomposition.
4.1. Effectofw,c,εwandεconfittedparameters
Coatedsampleswereprepared,andimpedancemeasurements wereperformedasdescribedinSection2.Foreachcombination of coating/electrolytic solution/immersion time the experimen-taldatawerecomparedwiththemodelshowninFig.1,usinga non-commercialsoftwaredevelopedattheLISECNRS,Paris.This
Fig.3.ComparisonoftheexperimentalimpedanceplotsobtainedwithsampleEexposedto0.5MNaCl,aftera48-himmersiontime,withthebestfittedcurvescorresponding tothecvaluesindicatedontheNyquistplot.
softwareallowedregressionofthemodelconsistingofa combina-tionofpassivecircuitelements,likeRpore,theelectrolyteresistance andtheCPEparametersrelevanttotheoxidefilm,andtheanalytical expressionofZc(ω),butdidnotprovideconfidenceintervalsforthe bestfittedparameters.Inourpreviouswork[7],itwasexplained that,owingtothequasi-capacitiveblockingbehaviourobserved atlowfrequency,theoxidefilmresistancecouldbeassumedto beverylargeandthereforeitsinclusionintheequivalentcircuit,in parallelwiththeCPE,wasnotnecessary.Equallyunnecessarywere circuitelementsaccountingforthecorrosionreactions,becauseno signofcorrosionwasobservedfortheimmersiontimesexplored inthepresentinvestigation.
In theregressionprocedure, , (ı)andRpore weretheonly adjustableparametersforthecoating;whereas,w,c,εwandεc weregivenfixedvalues(w=2.22×101cm,
c=2×1011cm,
εw=82 and εc=8). In our previouspaper [7] the effect of the assumedvaluesonthefittedparameterswasnotdiscussed.New dataandamoredetaileddiscussionarepresentedbelow.
4.1.1. Parametersεwandεc
Thepermittivities(εwandεc)areknownwithrathergood pre-cision;furthermore,ithasbeenshownthattheε()−profilesare quiteflatandthereforedonotaffecttheimpedanceofthesystem inasignificantway[9].
4.1.2. Parameterc
Theresistivityofthedrycoatingcislesswell-known.Thus, rec-ognizingthatitisimportanttoassessthemagnitudeofitseffect, themodelwasregressedtothesamesetofdatabyassumingin eachrunadifferentcvalue,coveringaratherwiderange.Fig.3 shows,asanexample,anexperimentalimpedanceplot,obtained withsampleE immersedin 0.5MNaClaftera 48-himmersion time,comparedwith7bestfitteddiagramscorrespondingtoc valuesvaryingfrom1010cmto2×1013cm.Inallcases,the
agreementbetweenexperimentalandcalculatedcurvesisgoodat allfrequencies(withsomedifferencesatfrequenciesabove5kHz where,asdiscussedabove,themodelisnotfullysatisfactory).Fig.4
showsthatthefittedparameters ,(ı)andRporedonotdepend oncinasignificantway,solongasc>5×1010cm.Many
poly-mericmaterialshavearesistivityhigherthanthisthresholdvalue
[14],possiblybysomeordersofmagnitude.Forexample,a resis-tivityof1×1015cmhasbeenreportedforadrynylonfilm[15].
Alltheresultspresentedinthefollowingsectionswereobtained byassumingc=2×1011cm,asinourpreviousstudy[7]andin
otherstudies[16].
4.1.3. Parameterw
Themostobviousassumptionaboutw,madebyourselvesin Ref.[7]andinthepresentstudyandbyotherauthors,e.g.[11], isthatitisidenticaltotheresistivityoftheelectrolyticsolution usedintheimpedancemeasurement.Thisimpliesthatthe com-positionof theelectrolyte insidetheporesshouldbe thesame as its bulk composition or, in otherwords that the water and theionsdissolvedinitbeincorporatedintothecoatingwithout anyselectivity.Resultspresentedintheliteratureshowthatsuch an assumptionmight not becorrect forall systems.For exam-ple,CastelaandSimoes[17]mentionthatthediffusivityofions islowerthanthatofwater;Huetal.[18]reportthatthe diffusiv-ityofchlorideioninepoxycoatingsisca.3ordersofmagnitude lowerthanthediffusivityofwater;and,accordingtoMiˇskovi ´c-Stankovi ´cetal.[11],theratiobetweenthediffusivitiesofwater andchlorideionisslightlyhigherthan10.Thus,wateruptakemay precedeionsuptake[11,12],and,solongasequilibriumisnotyet reached,thesolutionintheporesislikelytobelessconcentrated thantheoutersolution.Itisalsoquitepossiblethatthe compo-sitionoftheelectrolytewithintheporeswouldbeafunctionof immersiontime.Thechemicalnatureoftheelectrolyte,especially itsanion,mayhaveimportanteffects onthecoatingbehaviour.
1010 1011 1012 1013 0 1 2 3 4 5 γ / d im e n s io n le s s ρc / Ω cm
a
1010 1011 1012 1013 0.0 1.0x10-5 2.0x10-5 3.0x10-5 φ (δ ) / d im e n s io n le s s ρc / Ω cmb
1010 1011 1012 1013 0 1x105 2x105 3x105 4x105 5x105 Rp o re / Ω cm ρc / Ω cmc
Fig.4.Effectoftheassumedcvalueonthebestfittedparameters (a),(ı)(b)
andRpore(c).
Duarteetal.[19],usingnegative-feedbackscanning electrochem-ical microscope,have observed various topographic changes in coatingsduetothewateruptakeandtheingressofdissolvedions dependingontheelectrolytecomposition.
It isnoteworthythat thepermselectiveuptake of asolution lessconcentrated thanthebulksolutionwouldhave significant consequenceson(i)thedeterminationofthe()valuesand(ii) thecomparisonofdifferentelectrolytes.Sincecistypically8–10 ordersofmagnitudelargerthanw,Eq.(1)reducesto
()−1=−1w() (8)
already for very low () values. If an incorrectly low w is assumed,thewateruptakeisunderestimatedbythesamefactor,
1.0 0.8 0.6 0.4 0.2 0.0 104 105 106 107 108 109 1010 1011 1012 24 h 72 h 168 h
ρ
(
ξ
)
/
Ω
cm ξ / dimensionlessFig.5. ComparisonoftheresistivityprofilescalculatedforthecoatingE/NaCl solu-tionsystem,calculatedonthebasisoftotalwateruptake(emptysymbols)orwater uptakeinshortporesonly(fullsymbols).Immersiontimesareindicatedonthe figure.
becauselargeramountsoflessconcentratedelectrolyticsolution are required toachieve a fixed() value.The permselectivity effectsmaybemoreorlessmarkedfordifferentsaltsand,thus,may affecttheestimatedwateruptaketoadifferentextent.Miˇskovi ´c-Stankovi ´cetal.[12]reportedthatthewaterdiffusivityinepoxy coatingsdidnotdependonnatureoftheanion(chloride,sulfate, naphtol-3,6-disulphonate).Sincetheseanionshavethemselves dif-ferentdiffusivities,differentelectrolyteconcentrationsshouldbe foundintheporesofcoatingsimmersedinelectrolytesofthesame molarity,butwithdifferentanions.Inturn,differentelectrolyte concentrationswouldcausedifferentresistivityprofilesand dif-ferentimpedanceresponses.
4.2. Electrolyteinshortandthroughpores
The volume fraction of the electrolyte within the through pores,henceforthdenotedpore,wasdeterminedfordifferent coat-ing/electrolytecombinationsandvariousimmersiontimesusing Eq.(7)andthefittedRporevalues.Table1reports,asanexample, datarelevanttocoatingEin0.5MNaCl.Thesametablereportsalso thefittedparameters(ı), ,andRporeandthevolumefractionof theelectrolyteintheshortpores,averagedalongthecoating thick-nessı,henceforthdenotedav.Itmustbeemphasizedthat,ifwis underestimated,forthereasonsdiscussedintheprevioussection, bothporeandavwillbeunderestimatedbythesamefactor,and theirratiowillbecorrectlyassessed.InspectionofTable1shows that,forallimmersiontimes,av>pore,andthereforemostofthe electrolyteiscontainedinporesthatdonotreachthemetal. How-ever,thepore/avratioincreasesastheimmersiontimeincreases. Thissuggeststhat,forthissystem,astheimmersiontimeis pro-longedand thewateruptake progresses,(i)thenumber and/or diameteroftheporesincreasesand(ii)theporedepthincreases, suchthatanumberofshortporesbecomethroughporesatlonger immersiontime.Alltheseconclusionsagreewiththosedrawnby Miˇskovi ´c-Stankovi ´cetal.[11]fromtheanalysisofresultsofliquid sorptionandthermogravimetricexperiments.
Itisworthpointingoutthatthecalculationwasmadefor cylin-drical pores,perpendicular to the interfaces, which allows the volumeratioinEq.(7) tobereplacedbythesurfacearearatio. Clearly,realporesmustbetortuous.Consideringtheirtortuosity wouldaffectpore(becauseahighertortuositywouldcorrespond toahigherapparentıandthereforeahigherpore),butnotav (becauseEqs.(1)and(2)holdforanyporegeometry).Unless tortu-osityvaluesaremuchhigherthanafewunits,theconclusionthat av>porestillholds.
Table1
Dependenceofthefittedparameters(ı), andRporeandofthecalculatedquantitiesavandporeontheimmersiontimein0.5MNaClforcoatingE.
Immersiontimein0.5MNaCl/h (ı)/dimensionless /dimensionless Rpore/cm2 av/dimensionless pore/dimensionless
24 1.5×10−5 3.5 1.0×106 3.2×10−6 4.3×10−8 48 2.2×10−5 3.4 3.1×105 5.1×10−6 1.4×10−7 72 3.2×10−5 3.1 2.1×105 7.8×10−6 2.1×10−7 168 1.2×10−4 3.0 5.1×104 2.9×10−5 8.6×10−7 0 1x106 2x106 3x106 4x106 0 1x106 2x106 3x106 4x106 54 H z
-Z
''
/
Ωc
m
2Z
'
/
Ωcm
2 50 mHz 10-3 10-2 10-1 100 101 102 103 104 105 103 104 105 106 107|Z
|
/
Ωc
m
2f / Hz
10-3 10-2 10-1 100 101 102 103 104 105 0 30 60 90Sample E after 48 h in Na
2SO
4φ
/
°
f / Hz
Fig.6. ComparisonoftheexperimentalimpedanceplotsobtainedwithsampleEexposedto0.5MNa2SO4,aftera48-himmersiontime,withthebestfittedcurveobtained
byassumingw=22.2cm,c=2×1011cm,ε
w=82andεc=8.
Onceporeisknown,resistivityprofilestakingintoaccountthe electrolyteinallporesmaybecalculatedaccordingtoEq.(1),in which()isreplacedby′()definedas
′()=
pore+ (ı)
1+(ı)( −1) (9)
Fig.5comparesthesenew()−profiles (emptysymbols) withthose reported inFig. 10 of Ref.[7] (fullsymbols), which werecalculatedbydirectlyusingthefitted(ı)and valuesand neglectingtheelectrolyteinthethroughpores.Clearly,takingpore intoaccountaffects(ı)onlymarginally,thusthelowerresistivity limit(ı)isessentiallyidenticalinthisnewcalculationandinthe previousone.Instead,foreachimmersiontime,theresistivityat =0calculatedaccordingtoEqs.(1)and(9)andbasedon′()is
markedlylowerthanthatcalculatedaccordingtoEqs.(1)and(5)
andbasedon().
Additionaldifferencescausedbyusing′()insteadof()are:
(i)amoreextendedregionwhere()isindependentof,next tothecoating/oxideinterface,and (ii)aprogressivedecreaseof (0)withincreasingimmersiontime.Thepresenceofinnerand outerlayersinorganicfilmswasexperimentallyshownbyKittel etal.[20]whohighlightedtheheterogeneityofthepropertiesof coatingsalongtheirthickness.
InspectionofTable1showsthatthetotalwateruptake (aver-aged along thecoating thickness), given byav+pore,remains below10−4,i.e.below0.01%,evenafter168hofimmersion.Such
avalueissignificantlylowerthanvaluesoftenreportedinthe lit-eratureforvariouscoatingsmaterials(typicallybetween0.1%and 10%,seee.g.[11–13,19–22]).
Direct andreliable gravimetric datafor oursamplesarenot available.Inprevioussectionswediscussedreasonswhythewater uptakedatainTable1maybesignificantlyunderestimated. How-ever,itmustbestressedthat,althoughtheresultsofthefitting procedure are reported in part in terms of water uptake, e.g. (ı), what really matters is the conductivity, given by Eq. (1), and, with verygood approximation by Eq. (8). In the develop-mentofthepower-lawmodel(referredtoelectrolyte-penetrated coatings),()wasassumedtobedistributedalongthethickness accordingtoapowerlaw,andthecorrespondingresistivityand permittivitydistributionswerecalculatedaccordingly.Itmustbe realizedthat()isjustanintermediate inthecalculation.The modelmightbedirectlydescribedintermsof()andε(),both assumed to undergoa power-lawvariation, over a largeand a small(essentiallynegligible)range,respectively.Regressionwould thendirectlyprovide(ı)and values,allowingthecalculationof ()−profilesidenticaltothoseshowninthepresentpaper.In otherwords,thedetermined()−profiles,e.g.thoseinFig.5,are
reliable,whereasthe()−maybeornotreliable,dependingon permselectivityeffectsandonthepresence/absenceofsignificant amountsofpolymer-boundedwater.
Analyses ofthe water uptake basedonthe evolution ofthe coatingcapacitancewithimmersiontimeoftenleadtoits overesti-mation,byasmallfactor,ascomparedwithgravimetricmethods. Since the permittivity of water does not change dramatically withtheconcentrationofionsdissolvedinit,estimatesbasedon capacitanceareintrinsicallylesssensitivetoselectiveuptakeof water/ionsthanourapproachrelyingonresistivityvariations.
4.3. Effectofcoatingformulationandelectrolytecomposition
TheimpedanceofcoatingsEandOwasmeasuredduring immer-sionin0.5MNa2SO4,during168h,andanalyzedusingthemodel
describedinRef.[7],withthesameapproachasdescribedabove for coating Eexposed to0.5M NaCl.CoatingO, less protective than coatingE, wasnotstudied inNaCl solutionbecausesigns ofcorrosionappearedrathersoonand,toaccountforthe corro-sionprocess, theproposedmodelwould needtobecompleted byincludingeitheradditionalcircuitelementsoranappropriate analyticalexpression.
Theagreementbetweenexperimentsandmodelwasgoodfor allimmersion times,although,as discussedbefore, divergences appeared at frequencies higher than 1kHz (which were there-fore not taken into account in the fitting),as shown in Fig. 6.
Tables2and3summarizethefittingresults,whicharecompared tothoseforthecoatingE/NaClsysteminFig.7.Clearly,thedifferent coating/solution combinations showsignificantly different time dependenciesofbothRporeand(ı).ForcoatingE,uponincreasing theimmersiontime,RporedecreasesinNaClsolution,butincreases inNa2SO4solution.ForcoatingOinNa2SO4solution,Rpore under-goesonlysmallvariations,initiallydecreasingand thenslightly increasing.ForcoatingE,uponincreasingtheimmersiontime,(ı) increasesrapidlyinNaClsolutionandremainsroughlyconstantat amuchlowervalueinNa2SO4 solution.ForcoatingOinNa2SO4
solution,(ı)isinitiallymuchhigherthanforcoatingEandthen increasesslowlywhenimmersiontimeincreases.
TheseresultssuggestthatcoatingEisintrinsicallyless defec-tivethancoatingO,henceitslowerwateruptakeandsomewhat higherRporevalueatshortimmersiontime.CoatingOundergoes thenonlyminorchanges,i.e.itdoesnotuptakemuchadditional water, nor significantamounts of sulfate ions diffuse fromthe external solutiontothesolutionin thepores.CoatingE shows divergingbehaviour,dependingontheanioninthetestsolution. Supposingthattheamountofwateruptakenbythecoatingisnot
168 144 120 96 72 48 24 0 0 1x106 2x106 3x106 4x106
R
pore/
Ωcm
2Immersion time / h
Coating E / NaCl Coating E / Na2SO4 Coating O / Na2SO4a
168 144 120 96 72 48 24 0 2.0x10-5 4.0x10-5 6.0x10-5 8.0x10-5 1.0x10-4 1.2x10-4 Coating E / NaCl Coating E / Na2SO4 Coating O / Na2SO4 φ(δ)/ dimensionless
Immersion time / h
b
Fig.7.DependenceofRporeand(ı)ontheimmersiontimeforthecoating/solution
combinationsindicatedonthefigure.Thelinesareonlyanaidfortheeye.
dramatically differentin the two cases [12], theRpore decrease and(ı)decreasemightactuallybetheresultoftheprogressive increaseinthechlorideconcentrationinthepores(witha result-ingdecreaseinresistivity).Suchaneffectwouldnotbeobservedin sulfatesolution,duetoamuchslowerdiffusionofthisanion.The increaseinRpore valueswithexposuretime,observedinNa2SO4
solution,isnotacommonphenomenon,butincreasingimpedances have been observed in other studies [13,23]. To explain the
Table2
Dependenceofthefittedparameters(ı), andRporeandofthecalculatedquantitiesavandporeontheimmersiontimein0.5MNa2SO4forcoatingE.
Immersiontimein0.5MNa2SO4/h (ı)/dimensionless /dimensionless Rpore/cm2 av/dimensionless pore/dimensionless
6 2.3×10−6 3.6 8.5×105 5.3×10−7 3.9×10−8 24 3.9×10−6 4.0 1.9×106 8.0×10−7 1.8×10−8 48 1.6×10−6 3.9 2.5×106 3.5×10−7 1.3×10−8 72 3.8×10−6 4.2 2.9×106 7.9×10−7 1.1×10−8 168 2.2×10−6 4.2 2.9×106 4.4×10−7 1.1×10−8 Table3
Dependenceofthefittedparameters(ı), andRporeandofthecalculatedquantitiesavandporeontheimmersiontimein0.5MNa2SO4forcoatingO.
Immersiontimein0.5MNa2SO4/h (ı)/dimensionless /dimensionless Rpore/cm2 av/dimensionless pore/dimensionless
6 3.7×10−5 3.9 6.7×105 7.7×10−6 4.9×10−8 24 2.8×10−5 3.4 6.7×105 6.5×10−6 5.0×10−8 48 4.3×10−5 3.4 5.4×105 9.8×10−6 6.2×10−8 120 4.4×10−5 3.2 7.8×105 1.0×10−5 4.3×10−8 144 5.2×10−5 3.3 8.3×105 1.2×10−5 4.0×10−8 168 5.3×10−5 3.3 9.5×105 1.2×10−5 3.5×10−8
experimentalobservations,eitherafurtherwater-induced cross-linkingofthecoatingmaterialor,lessprobably,aporeshrinkingas aconsequenceofcoatingswellingmaybehypothesized. Indepen-dentevidenceallowingtoassesswhichphenomenonpredominates isnotavailable.
5. Conclusions
The“power-lawmodel”, whose applicationtoanti-corrosion coatingshad been proposedin Ref. [7], hasbeenrevisited and employedtoanalyzenewexperimentaldata.
Ithasbeenshownthataninaccurateknowledgeoftheresistivity ofthedrycoatingmaterialcisunlikelytoaffectthequalityofthe agreementbetweenmodelandexperimentaldata,northevaluesof theregressedparameters,atleastaslongascislarge.Instead,an erroneousassumptionabouttheresistivityoftheelectrolyte(w) withinthecoatingporeshasamajorimpactontheestimatedwater uptake.If,asithasbeenoftenreported,thediffusionofionsinto thecoatingisslowerthatwaterdiffusion,thenbothwandwill beunderestimated,possiblybyalargefactor.
Theeffectof“throughpores”and“shortpores”hasbeentaken simultaneouslyintoaccounttocalculateresistivityprofiles.
Finally,itwasshownthattheevolutionofthecoatingproperties withimmersiontimedependsbothonthecoatingmaterial,e.g. onitsmicrostructure,andontheelectrolyte,e.g.theabilityofits anionstodiffuseintothecoating.
Acknowledgments
Theexperimentaldatawereobtainedintheframeworkofthe SMILEproject(SurfaceMonoInnovativeLayerforEnvironment), withthefinancialsupportoftheDGCIS(DirectionGénéraledela Compétitivité,del’IndustrieetdesServices).N.Pébèrethanksthe partnersoftheproject:Mapaero(Pamiers),Rescoll(Bordeaux), Air-bus(Toulouse),Dassault(Paris),EADSIW(Suresnes),l’Electrolyse (Bordeaux),and thelaboratoriesLCPOand US2B(Universitéde Bordeaux).
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